US3669853A - Coumarin-carrier addition agent for nickel baths - Google Patents
Coumarin-carrier addition agent for nickel baths Download PDFInfo
- Publication number
- US3669853A US3669853A US842027A US3669853DA US3669853A US 3669853 A US3669853 A US 3669853A US 842027 A US842027 A US 842027A US 3669853D A US3669853D A US 3669853DA US 3669853 A US3669853 A US 3669853A
- Authority
- US
- United States
- Prior art keywords
- coumarin
- addition agent
- nickel
- bath
- improvement
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 title claims abstract description 54
- 229910052759 nickel Inorganic materials 0.000 title claims abstract description 27
- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 23
- ZYGHJZDHTFUPRJ-UHFFFAOYSA-N coumarin Chemical compound C1=CC=C2OC(=O)C=CC2=C1 ZYGHJZDHTFUPRJ-UHFFFAOYSA-N 0.000 claims abstract description 96
- 229960000956 coumarin Drugs 0.000 claims abstract description 48
- 235000001671 coumarin Nutrition 0.000 claims abstract description 48
- 238000007747 plating Methods 0.000 claims abstract description 24
- 239000000203 mixture Substances 0.000 claims abstract description 21
- 239000012876 carrier material Substances 0.000 claims abstract description 15
- 238000004070 electrodeposition Methods 0.000 claims abstract description 4
- GOLORTLGFDVFDW-UHFFFAOYSA-N 3-(1h-benzimidazol-2-yl)-7-(diethylamino)chromen-2-one Chemical compound C1=CC=C2NC(C3=CC4=CC=C(C=C4OC3=O)N(CC)CC)=NC2=C1 GOLORTLGFDVFDW-UHFFFAOYSA-N 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 5
- 238000005282 brightening Methods 0.000 claims description 4
- 239000003463 adsorbent Substances 0.000 claims description 3
- 150000002815 nickel Chemical class 0.000 claims description 3
- 238000010298 pulverizing process Methods 0.000 claims description 3
- 239000011260 aqueous acid Substances 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- 239000000463 material Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 239000010425 asbestos Substances 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 229910052895 riebeckite Inorganic materials 0.000 description 3
- 239000005909 Kieselgur Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000009713 electroplating Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 206010067484 Adverse reaction Diseases 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 235000010582 Pisum sativum Nutrition 0.000 description 1
- 240000004713 Pisum sativum Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000006838 adverse reaction Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- -1 boric acid Chemical class 0.000 description 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- 239000006172 buffering agent Substances 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000010705 motor oil Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/12—Process control or regulation
- C25D21/14—Controlled addition of electrolyte components
Definitions
- This invention relates to coumarin compositions as addition agents for use in nickel electroplating baths.
- coumarin as an addition agent to improve brightening and leveling properties of the electrodeposited nickel in a nickel plating bath is well established in commercial plating operations.
- the coumarin may be incorporated as the sole brightening agent in an acid nickel bath of the Watts type containing a soluble nickel salt and a buffering agent such as boric acid, or these baths may contain additional organic brighteners selected from a wide variety of compounds, as described in prior patents.
- Typical nickel baths containing coumarin with and without additional brighteners are disclosed for example in U.S. Pat. Nos. 2,579,636 and 2,634,076.
- the solubility of coumarin in the acid nickel plating solution is quite limited, normally on the order of one-half gram per liter of solution, and since it is plated out of solution fairly rapidly, it must be replaced regularly, preferably continuously, during the plating operation. It is conventional to control the coumarin level in the bath by circulating the plating solution, or part of it, through a filter into which the coumarin has been charged. Initially, the matter of getting sufficient coumarin into the plating solution in this way presents no great problem if an excess is used; however other problems arise due to this excess if the plating bath temperature approaches or exceeds the melting point of the coumarin.
- the substantially increased porous or fibrous surface area over which the coumarin is distributed in the coumarin-carrier combination is responsible for suppressing the formation of the undesirable, insoluble form of the coumarin by keeping the coumarin particles physically separated.
- This property of the carrier also serves to promote quicker dissolution of the coumarin, as demonstrated by analytical test, and thus eliminates the need to use excessive amounts of coumarin initially to achieve a desired solution concentration.
- the coumarin-carrier composition is readily prepared by heating the coumarin on a steam bath until it becomes fluid, and while in this state a powdered carrier material is stirred in until the molten coumarin is taken up and a granular composition is obtained. Greater amounts of carrier relative to coumarin will of course produce a drier, more granular composition.
- Various materials may be used as the carrier, the essential requirements being that it be insoluble in the acid nickel bath; also it be of solid, porous nature to permit absorption or adsorption of coumarin and that the resulting composition be friable rather than plastic or waxy so that it can be crushed or pulverized.
- Typical carrier materials that are useful include filter aids; e.g. a fluffy, insoluble, cellulosic material, either of alpha or beta-cellulose form; asbestos or other siliceous compounds; also diatomaceous earth and carbonaceous material such as graphite or powdered charcoal. Mixtures of these can also be used.
- the carrier material must be one which is virtually insoluble in the acid plating bath and does not cause an adverse reaction in the bath.
- a preferred addition composition is prepared by melting coumarin as described above and stirring into it while in the molten state sufiicient fluffy cellulosic filter aid to adsorb all of the molten coumarin. At this point the mixture becomes nearly dry and forms large granules about the size of peas.
- the preferred ratio of coumarin to filter aid in this composition is found to be about 5 parts to l, by weight, but satisfactory results are obtained within a range of weight ratios of from about 3:1 to 7:1.
- the resulting granules are ball-milled or otherwise pulverized. It can then be packed into the plating bath recirculation filter in the usual way.
- An addition agent for an aqueous nickel electrodeposition bath which comprises a finely comminuted or powdered composition prepared by pulverizing the solidified admixture of molten coumarin and an adsorbent particulate carrier material non-reactive with said coumarin.
- aqueous acid bath for the electrodeposition of nickel plate wherein said bath contains at least one soluble nickel salt as the salt as the source of the nickel and at least one organic brightening agent which always includes coumarin, the improvement wherein a powdered composition, prepared by pulverizing the solidified admixture of molten coumarin and an adsorbent particulate carrier material nonreactive with said coumarin, is present in said bath.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Automation & Control Theory (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electroplating And Plating Baths Therefor (AREA)
Abstract
An improved coumarin addition agent is disclosed for use in nickel electrodeposition baths, wherein the coumarin is adsorbed on a bath-insoluble, friable, porous carrier material to produce a composition adapted to be placed in the filter commonly employed in plating baths.
Description
United States Patent Beach 1 June 13, 1972 COUMARIN-CARRIER ADDITION AGENT FOR NICKEL BATHS [72] Inventor: Sidney C. Beach, Cleveland, Ohio [73] Assignee: Chemetron Corporation, Chicago, 111.
[22] Filed: July 15, 1969 [21] Appl. No.: 842,027
[52] U.S. C1. 204/49, 204/D1G. 2, 204/235, 204/238, 204/240, 204/276 [51] Int. Cl ..C23b 5/08, C23b 5/46, BOlk 3/00 [58] Field of Search ..204/49, 235, 238, 240, 276,
204/DIG. 2, 45 R [56] References Cited UNITED STATES PATENTS 2.809.187 10/1957 Chapin et a1 ..260/88.1 3.245.886 4/1966 Michael ..204/49 X FOREIGN PATENTS OR APPLICATIONS 1,094,184 12/1967 Great Britain ..204/49 507,577 11/1954 Canada ..204/49 144,685 3/1962 U.S.S.R. "204/49 OTHER PUBLlCATIONS A. Kenneth Graham, Electroplating Engineering Handbook, pp. 605- 607, (1955).
Primary Examiner-G. L. Kaplan Attorney-Steward & Steward, Merrill F. Steward, Donald T. Steward and Walter D. Hunter 57] ABSTRACT 10 Claims, No Drawings COUMARlN-CARRIER ADDlTION AGENT FOR NICKEL BATHS This invention relates to coumarin compositions as addition agents for use in nickel electroplating baths.
The use of coumarin as an addition agent to improve brightening and leveling properties of the electrodeposited nickel in a nickel plating bath is well established in commercial plating operations. The coumarin may be incorporated as the sole brightening agent in an acid nickel bath of the Watts type containing a soluble nickel salt and a buffering agent such as boric acid, or these baths may contain additional organic brighteners selected from a wide variety of compounds, as described in prior patents. Typical nickel baths containing coumarin with and without additional brighteners are disclosed for example in U.S. Pat. Nos. 2,579,636 and 2,634,076.
As is discussed in such patents, the solubility of coumarin in the acid nickel plating solution is quite limited, normally on the order of one-half gram per liter of solution, and since it is plated out of solution fairly rapidly, it must be replaced regularly, preferably continuously, during the plating operation. It is conventional to control the coumarin level in the bath by circulating the plating solution, or part of it, through a filter into which the coumarin has been charged. Initially, the matter of getting sufficient coumarin into the plating solution in this way presents no great problem if an excess is used; however other problems arise due to this excess if the plating bath temperature approaches or exceeds the melting point of the coumarin.
Coumarin melts at 152 to 154 F; however at somewhat lower temperature and well within the usual operating temperature range of 135 to 140 F. for nickel plating baths, coumarin becomes either very tacky or melts sufiiciently to cause the formation of large thick flakes or lumps that are as hard as concrete and virtually insoluble. A small percentage does dissolve slowly but the efficiency of the system is substantially reduced. A large part of this hardened material must therefore frequently be discarded from the filter and replaced with a fresh, more efficient charge. The result is that substantial amounts of coumarin are lost when the filter is cleaned and repacked.
There is also another problem. With an excess of coumarin in the filter and with various amounts of it in the form that resists dissolution, extreme care must be exercised to see that the temperature of the plating bath is never allowed to go above the true melting point of the coumarin. Because of the normally small differential between optimum plating bath temperature and the melting point of coumarin, this presents particular difficulty in most commercial operations, especially during summer months or where heat exchangers are used in conjunction with the filter. If the coumarin in the filter actually melts to liquid state, it will escape and enter the plating solution as a separate oily phase rather than in dissolved form, and this will produce large pits in the nickel deposit similar to those obtained if the solution were contaminated with motor oil.
lt has now been found that most of the foregoing difficulty in the use of coumarin as an addition agent in nickel plating baths can be avoided. This is accomplished by dissolving the coumarin into the bath from a finely comminuted or powdered composition consisting of coumarin and an inert porous carrier material on which the coumarin has been adsorbed. This coumarin-carrier composition, when incorporated in the plating bath filter. substantially resists any tendency of the coumarin to form either of the hard flaky form or oily phases mentioned above. It is presently assumed that the substantially increased porous or fibrous surface area over which the coumarin is distributed in the coumarin-carrier combination is responsible for suppressing the formation of the undesirable, insoluble form of the coumarin by keeping the coumarin particles physically separated. This property of the carrier also serves to promote quicker dissolution of the coumarin, as demonstrated by analytical test, and thus eliminates the need to use excessive amounts of coumarin initially to achieve a desired solution concentration.
The coumarin-carrier composition is readily prepared by heating the coumarin on a steam bath until it becomes fluid, and while in this state a powdered carrier material is stirred in until the molten coumarin is taken up and a granular composition is obtained. Greater amounts of carrier relative to coumarin will of course produce a drier, more granular composition. Various materials may be used as the carrier, the essential requirements being that it be insoluble in the acid nickel bath; also it be of solid, porous nature to permit absorption or adsorption of coumarin and that the resulting composition be friable rather than plastic or waxy so that it can be crushed or pulverized.
Typical carrier materials that are useful include filter aids; e.g. a fluffy, insoluble, cellulosic material, either of alpha or beta-cellulose form; asbestos or other siliceous compounds; also diatomaceous earth and carbonaceous material such as graphite or powdered charcoal. Mixtures of these can also be used. Obviously the carrier material must be one which is virtually insoluble in the acid plating bath and does not cause an adverse reaction in the bath.
A preferred addition composition is prepared by melting coumarin as described above and stirring into it while in the molten state sufiicient fluffy cellulosic filter aid to adsorb all of the molten coumarin. At this point the mixture becomes nearly dry and forms large granules about the size of peas. The preferred ratio of coumarin to filter aid in this composition is found to be about 5 parts to l, by weight, but satisfactory results are obtained within a range of weight ratios of from about 3:1 to 7:1. When the mixture is fully cooled, the resulting granules are ball-milled or otherwise pulverized. It can then be packed into the plating bath recirculation filter in the usual way.
As mentioned above, other carrier materials may be employed and asbestos fiber ranks second to the preferred cellu losic filter aid material. Because of lower porosity of the asbestos, the weight ratio of coumarin to carrier in this case is lower, being on the order of about 4:1 for best results. Similarly, diatomaceous earth exhibits lower porosity and an optimum ratio is about 3:1 in this case. Ratios up to as much as 7:1 of these materials are also possible, but the benefits of the composition are reduced.
What is claimed is:
1. An addition agent for an aqueous nickel electrodeposition bath, which comprises a finely comminuted or powdered composition prepared by pulverizing the solidified admixture of molten coumarin and an adsorbent particulate carrier material non-reactive with said coumarin.
2. An addition agent as defined in claim 1, wherein said carrier material is selected from the group consisting of cellulosic, siliceous and carbonaceous solids and mixtures thereof.
3. An addition agent as defined in claim 2, wherein the weight ratio of coumarin to carrier is the range of from about 3:1 to 7: l
4. An addition agent as defined in claim 3, which consiss essentially of coumarin and cellulosic filter aid.
5. An addition agent as defined in claim 4, wherein the weight ratio is about 5: 1.
6. In an aqueous acid bath for the electrodeposition of nickel plate, wherein said bath contains at least one soluble nickel salt as the salt as the source of the nickel and at least one organic brightening agent which always includes coumarin, the improvement wherein a powdered composition, prepared by pulverizing the solidified admixture of molten coumarin and an adsorbent particulate carrier material nonreactive with said coumarin, is present in said bath.
7. The improvement in a nickel plating bath as defined in claim 6, wherein said carrier material is selected from the group consisting of cellulosic, siliceous and carbonaceous solids and mixtures thereof.
8. The improvement in a nickel plating bath as defined in claim 7, wherein the weight ratio of coumarin to carrier material is in the range of from about 3:1 to 7: 1.
9. The improvement in a nickel plating bath as defined in claim 8, wherein the addition agent consists essentially of coumarin and cellulosic filter aid.
10. The improvement in a nickel plating bath as defined in claim 9. wherein said addition agent comprises coumarin and 5 cellulosic filter aid in a weight ratio of about 5:1.
t a a:
Claims (9)
- 2. An addition agent as defined in claim 1, wherein said carrier material is selected from the group consisting of cellulosic, siliceous and carbonaceous solids and mixtures thereof.
- 3. An addition agent as defined in claim 2, wherein the weight ratio of coumarin to carrier is the range of from about 3:1 to 7:
- 4. An addition agent as defined in claim 3, which consists essentially of coumarin and cellulosic filter aid.
- 5. An addition agent as defined in claim 4, wherein the weight ratio is about 5:1.
- 6. In an aqueous acid bath for the electrodeposition of nickel plate, wherein said bath contains at least one soluble nickel salt as the salt as the source of the nickel and at least one organic brightening agent which always includes coumarin, the improvement wherein a powdered composition, prepared by pulverizing the solidified admixture of molten coumarin and an adsorbent particulate carrier material non-reactive with said coumarin, is present in said bath.
- 7. The improvement in a nickel plating bath as defined in claim 6, wherein said carrier material is selected from the group consisting of cellulosic, siliceous and carbonaceous solids and mixtures thereof.
- 8. The improvement in a nickel plating bath as defined in claim 7, wherein the weight ratio of coumarin to carrier material is in the range of from about 3:1 to 7:1.
- 9. The improvement in a nickel plating bath as defined in claim 8, wherein the addition agent consists essentially of coumarin and cellulosic filter aid.
- 10. The improvement in a nickel plating bath as defined in claim 9, wherein said addition agent comprises coumarin and cellulosic filter aid in a weight ratio of about 5:1.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US84202769A | 1969-07-15 | 1969-07-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3669853A true US3669853A (en) | 1972-06-13 |
Family
ID=25286350
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US842027A Expired - Lifetime US3669853A (en) | 1969-07-15 | 1969-07-15 | Coumarin-carrier addition agent for nickel baths |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3669853A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2311110A1 (en) * | 1975-05-16 | 1976-12-10 | M & T Chemicals Inc | PROCESS FOR THE ELECTROLYTIC DEPOSIT OF NICKEL, COBALT AND THEIR ALLOY WITH IRON |
| US4532887A (en) * | 1983-05-02 | 1985-08-06 | General Motors Corporation | Life extension of catalyst predip baths |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA507577A (en) * | 1954-11-23 | Weisberg Louis | Electrodeposition of metals | |
| US2809187A (en) * | 1954-11-01 | 1957-10-08 | Monsanto Chemicals | Styrene copolymers |
| SU144685A1 (en) * | 1961-03-21 | 1961-11-30 | Г.Ф. Воробьева | Self-regulating leveling nickel electrolyte |
| US3245886A (en) * | 1961-08-10 | 1966-04-12 | Dehydag Gmbh | Electroplating process and self-regulating electroplating baths therefor |
| GB1094184A (en) * | 1964-03-13 | 1967-12-06 | Wilmot Breeden Ltd | Improvements in or relating to the electro-deposition of metals |
-
1969
- 1969-07-15 US US842027A patent/US3669853A/en not_active Expired - Lifetime
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA507577A (en) * | 1954-11-23 | Weisberg Louis | Electrodeposition of metals | |
| US2809187A (en) * | 1954-11-01 | 1957-10-08 | Monsanto Chemicals | Styrene copolymers |
| SU144685A1 (en) * | 1961-03-21 | 1961-11-30 | Г.Ф. Воробьева | Self-regulating leveling nickel electrolyte |
| US3245886A (en) * | 1961-08-10 | 1966-04-12 | Dehydag Gmbh | Electroplating process and self-regulating electroplating baths therefor |
| GB1094184A (en) * | 1964-03-13 | 1967-12-06 | Wilmot Breeden Ltd | Improvements in or relating to the electro-deposition of metals |
Non-Patent Citations (1)
| Title |
|---|
| A. Kenneth Graham, Electroplating Engineering Handbook, pp. 605 607, (1955). * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2311110A1 (en) * | 1975-05-16 | 1976-12-10 | M & T Chemicals Inc | PROCESS FOR THE ELECTROLYTIC DEPOSIT OF NICKEL, COBALT AND THEIR ALLOY WITH IRON |
| US4532887A (en) * | 1983-05-02 | 1985-08-06 | General Motors Corporation | Life extension of catalyst predip baths |
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